EP0495453A1 - Tube pour la transmission de chaleur - Google Patents
Tube pour la transmission de chaleur Download PDFInfo
- Publication number
- EP0495453A1 EP0495453A1 EP92100503A EP92100503A EP0495453A1 EP 0495453 A1 EP0495453 A1 EP 0495453A1 EP 92100503 A EP92100503 A EP 92100503A EP 92100503 A EP92100503 A EP 92100503A EP 0495453 A1 EP0495453 A1 EP 0495453A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- grooves
- heat transmission
- tube body
- tube
- transmission tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 230000005540 biological transmission Effects 0.000 title claims abstract description 42
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- 239000010936 titanium Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 239000000463 material Substances 0.000 claims 1
- 230000004907 flux Effects 0.000 abstract description 14
- 239000002826 coolant Substances 0.000 description 12
- 238000009835 boiling Methods 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 244000287353 Crassocephalum crepidioides Species 0.000 description 1
- 206010016322 Feeling abnormal Diseases 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/18—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
- F28F13/185—Heat-exchange surfaces provided with microstructures or with porous coatings
- F28F13/187—Heat-exchange surfaces provided with microstructures or with porous coatings especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
- F28F1/26—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means being integral with the element
Definitions
- the present invention relates to a heat transmission tube, and more specifically to that built in an evaporator of a freezer, a coolant being boiled at the outer surface of which when the tube is used.
- the heat transmission tube disclosed in Published Unexamined Japanese Patent Application (PUJPA) No. 57-131992 can be named as a typical conventional tube which boils coolant brought into contact with the outer surface thereof through exchange of heat between the coolant and fluid in the tube, so as to enhance transmission of heat propagated on to coolant (to be called boiling heat transmission hereinafter).
- a heat transmission tube is characterized by having a first and second groove portion formed on the outer surface of the low-fin tube by a roll forming process.
- This type of heat transmission tube is used in a liquid or gaseous coolant.
- This tube exhibits a good property in terms of heat transmission rate since, in the tube, bubbles remaining in the groove make boiling continue, thereby increasing the amount of heat transmission. Thus, a high transmissibility can be achieved.
- the purpose of the invention is to provide a heat transmission tube which exhibits a high and stable heat transmissibility in both cases of low and high heat fluxes.
- a heat transmission tube having a tube body, first grooves formed at a predetermined pitch therebetween on an outer surface of the tube body continuously along a circumferential direction, the first grooves open to an outside, and having an opening space, a width of which is narrower than that of a bottom space thereof, and second grooves formed at a predetermined pitch therebetween on the outer surface of the tube body continuously along an axial direction, the second grooves having a depth shallower than that of the first grooves, and connecting opening spaces of adjacent first grooves to each other, wherein a projecting member is provided on a bottom surface of each of the first grooves so as to connect a side wall of each of the first grooves to another.
- Fig. 1 is a partial perspective view of a heat transmission tube according to an embodiment of the present invention.
- This figure shows a part of a tube body 10, in which fluid, i.e. water, coolant such as Freon, or vapor thereof, flows.
- fluid i.e. water, coolant such as Freon, or vapor thereof
- continuous second grooves 12 are formed also on the outer surface of the tube body 10 along the axial direction thereof (indicated by letter B in the figure).
- a projecting member 15 for connecting a side wall 14 of one of the first grooves 11 to the same of another.
- some of the examples of the raw materials for the tube body 10 are copper, steel, titanium, aluminum, and an alloy thereof.
- Each of the first grooves 11 has a bottom portion 16 a width W1 of which is relatively wide, and an opening portion 17 a width W2 of which is relatively narrow.
- the ratio of the width of the bottom portion 16 to that of the opening portion 17 (W1/W2) should preferably be in the range between 1 and 12 in consideration of follow-up for capturing and departure of bubbles.
- a pitch P1 of the first grooves 11, that is, the distance between the centers of adjacent first grooves 11, should preferably be in the range between 0.5 mm and 1.0 mm in consideration of follow-up for capturing of bubbles and the heat transmissibility.
- the number of the first grooves 11 should preferably be 25-50 per an inch, and they should be formed all the way through the heat transmission tube with an appropriate pitch P1 between each adjacent pair of the grooves.
- a depth D1 of each of the first grooves 11 should preferably be in the range between 0.2 mm and 1.2 mm in consideration of follow-up for capturing of bubbles and the heat transmissibility. It should be noted here that as long as formed continuously in the circumferential direction of the tube body 10, the first grooves 11 may be ring-shaped, or spiral.
- a pitch P2 of the second grooves 12, that is, the distance between the centers of adjacent second grooves 12, should preferably be in the range between 0.4 mm and 1.5 mm. This is because, if the pitch P2 is out of this range, the opening portion 17 cannot be formed to have desired measurements due to structural limitation.
- the number of the second grooves 12 should preferably be 25-60 per an inch, and they should be formed all the way through the heat tube with an appropriate pitch P2 between each adjacent pair of the grooves. In order to generate more bubbles, the number of the opening portions 17 and the second grooves should be increased. It should be noted, however, that the number of these portions and grooves is somehow limited by the type of the fluid brought into contact with the outer surface of the tube body.
- a height H of the projecting member 15 should preferably be 2-40% of the depth 1 of the first grooves 11. This is because, if the height H is less than 2% of the depth D1, the heat transmission tube cannot exhibit its full heat transmissibility in a low heat flux region, and if the height H exceeds 40% of the depth D1, supply of the coolant to the outer surface of the tube body is significantly reduced in a high heat flux region. Most preferably, the height H should be 10-40% of the depth D1. Further, as shown in Fig. 2, a pitch P3 of the projecting members 15, that is, the distance between the tip ends of adjacent projecting members should preferably be in the range between 0.5-4.5 mm.
- the shape of the cross section of the projecting member 15 is not particularly specified here, and may be, for example, polygonal such as triangular, semicircular, or trapezoidal.
- the heat transmission tube has such a structure that a projecting member 15 is formed on the bottom of each of the first grooves 11; therefore the area of the outer surface, which is called heat transmission area, with which the coolant is brought into contact, is larger than that without any projecting member.
- the area of the outer surface, which is called heat transmission area, with which the coolant is brought into contact is larger than that without any projecting member.
- each of the projecting members 15 serves to divide the bottom space of each of the first grooves 11 into small regions; therefore it becomes pos sible to suppress movement of the coolant at each proximal fin, that is, the bottom space of each of the first grooves.
- coolant can be easily boiled by regional heating of the outer surface of the tube body; therefore the tube can exhibit a high heat transmissibility improved especially in a low heat flux region.
- a copper tube having the external diameter of 19.05 mm and the thickness of 1.24 mm is subjected to a process with a disk 30 for formation of fins, disk 33 for formation of projecting members, tool 35 for formation of a second grooves, and rolling tools 36-39, as can be seen in Fig. 3.
- the process of the tube body 31 is held by mandrel 41 in the tube and carried out starting from the state shown on the left-hand side of the figure toward the right-hand side.
- the outer surface of the tube body 31 is formed into fins 32, and a projecting member 34 is formed on the bottom portion of each of the first grooves 40, each defined by adjacent fins 32, by means of a formation disk 33, on a part of the circumference of which teeth 33a are formed as shown in Fig. 4.
- the tip of each of the fins 32 is gradually pressed to have thick head portion shown in the figure, and the second grooves are formed on the tube body 31 along the axial direction thereof by use of the rolling tube 35, in particular.
- the tube thus obtained has forty of the first grooves 40 formed on each one-inch portion of the outer surface of the tube body 31 along the circumferential direction, a projecting member 34 formed on the bottom of each of the first grooves 40 along a direction substantially parallel to the axial direction of the tube body 31 such that the member 34 connect the fins 32 on both sides thereof to each other, and eighty of the second grooves formed also on the outer surface of the tube body along the axial direction thereof.
- Each of each of the first grooves has the following measurements; the width of the bottom portion of 0.3 mm, the width of the opening portion of 0.1 mm, and the depth of 0.7 mm.
- the pitch of the first grooves is 0.64 mm.
- the pitch of the second grooves is 0.75 mm.
- the height of the projecting members is 15% of the depth of the first grooves.
- the pitch of the tip portions of the projecting members is 1.5 mm, and the cross section of each of the projecting members is essentially triangular.
- Fig. 5 shows the boiling heat transmissibility (defined by the amount of heat transmitted, per unit length, unit time, and unit temperature) exhibited from a low heat flux region to a high heat flux region of each of the heat transmission tube of the present invention (characteristic curve 3), a conventional heat transmission tube with first and second grooves and without projecting members (curve 2), and a conventional heat transmission tube with low fin (26 per inch) (curve 1).
- the heat transmission tube of the present invention exhibits a high boiling heat transmissibility in both low and high heat flux regions.
- the transmissibility of the tube of the invention is 20% higher than that of the conventional tube (curve 2).
- the projecting members 60 are formed such that the cross section thereof has a triangular shape as shown in Fig. 6B, but the shape of the cross section may be trapezoidal or semicircular as shown in Figs. 6A and 6C, without degrading the advantage of the invention.
- the projecting members 60 are formed along a direction substantially parallel to the axial direction of the tube body, but as long as the projecting members connect both side walls of each of the first grooves to each other, they may be formed such that the longitudinal direction of the projecting members 70 is tilted with respect to the axial direction (direction C in Fig. 8) of the tube body by a predetermined angle less than 60° as can be seen in Figs. 7 and 8.
- the heat transmission tube of the present invention has a high and stable heat transmissibility in both cases of low and high heat fluxes.
- heat exchangers in which the heat transmission tube of the present invention is employed have advantages in terms of miniaturization of the device, as well as performance.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Shaping Metal By Deep-Drawing, Or The Like (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14857/91 | 1991-01-14 | ||
JP3014857A JP2788793B2 (ja) | 1991-01-14 | 1991-01-14 | 伝熱管 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0495453A1 true EP0495453A1 (fr) | 1992-07-22 |
EP0495453B1 EP0495453B1 (fr) | 1994-04-06 |
Family
ID=11872702
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP92100503A Revoked EP0495453B1 (fr) | 1991-01-14 | 1992-01-14 | Tube pour la transmission de chaleur |
Country Status (5)
Country | Link |
---|---|
US (1) | US5186252A (fr) |
EP (1) | EP0495453B1 (fr) |
JP (1) | JP2788793B2 (fr) |
KR (1) | KR940007194B1 (fr) |
DE (1) | DE69200089T2 (fr) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0559599A1 (fr) * | 1992-03-02 | 1993-09-08 | Carrier Corporation | Tube pour échangeur de chaleur |
EP0607839A1 (fr) * | 1993-01-22 | 1994-07-27 | Wieland-Werke Ag | Tube pour échange de chaleur, procédé de fabrication et utilisation d'un tel tube |
CN101776412A (zh) * | 2010-03-02 | 2010-07-14 | 金龙精密铜管集团股份有限公司 | 蒸发传热管 |
CN101532795B (zh) * | 2008-03-12 | 2013-07-24 | 威兰德-沃克公开股份有限公司 | 金属热交换管 |
WO2014072046A1 (fr) * | 2012-11-12 | 2014-05-15 | Wieland-Werke Ag | Tube de transfert de chaleur par évaporation doté d'une cavité creuse |
WO2015128061A1 (fr) * | 2014-02-27 | 2015-09-03 | Wieland-Werke Ag | Tube d'échangeur de chaleur métallique |
Families Citing this family (55)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR0132015B1 (ko) * | 1993-02-24 | 1998-04-20 | 가나이 쯔도무 | 열 교환기 |
ES2171519T3 (es) * | 1994-11-17 | 2002-09-16 | Carrier Corp | Tubo de transferencia de calor. |
CA2161296C (fr) * | 1994-11-17 | 1998-06-02 | Neelkanth S. Gupte | Tube de transfert thermique |
US5697430A (en) * | 1995-04-04 | 1997-12-16 | Wolverine Tube, Inc. | Heat transfer tubes and methods of fabrication thereof |
JP3303599B2 (ja) * | 1995-05-17 | 2002-07-22 | 松下電器産業株式会社 | 伝熱管 |
US6197180B1 (en) | 1996-02-09 | 2001-03-06 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | High aspect ratio, microstructure-covered, macroscopic surfaces |
US5681661A (en) * | 1996-02-09 | 1997-10-28 | Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College | High aspect ratio, microstructure-covered, macroscopic surfaces |
US5996686A (en) * | 1996-04-16 | 1999-12-07 | Wolverine Tube, Inc. | Heat transfer tubes and methods of fabrication thereof |
US6176302B1 (en) * | 1998-03-04 | 2001-01-23 | Kabushiki Kaisha Kobe Seiko Sho | Boiling heat transfer tube |
US6935409B1 (en) | 1998-06-08 | 2005-08-30 | Thermotek, Inc. | Cooling apparatus having low profile extrusion |
US7147045B2 (en) * | 1998-06-08 | 2006-12-12 | Thermotek, Inc. | Toroidal low-profile extrusion cooling system and method thereof |
US6176301B1 (en) * | 1998-12-04 | 2001-01-23 | Outokumpu Copper Franklin, Inc. | Heat transfer tube with crack-like cavities to enhance performance thereof |
US6981322B2 (en) | 1999-06-08 | 2006-01-03 | Thermotek, Inc. | Cooling apparatus having low profile extrusion and method of manufacture therefor |
US7305843B2 (en) | 1999-06-08 | 2007-12-11 | Thermotek, Inc. | Heat pipe connection system and method |
DE19945581B4 (de) * | 1999-09-23 | 2014-04-03 | Alstom Technology Ltd. | Turbomaschine |
US6462949B1 (en) | 2000-08-07 | 2002-10-08 | Thermotek, Inc. | Electronic enclosure cooling system |
US6760972B2 (en) | 2000-09-21 | 2004-07-13 | Packless Metal Hose, Inc. | Apparatus and methods for forming internally and externally textured tubing |
US6488079B2 (en) | 2000-12-15 | 2002-12-03 | Packless Metal Hose, Inc. | Corrugated heat exchanger element having grooved inner and outer surfaces |
DE10101589C1 (de) * | 2001-01-16 | 2002-08-08 | Wieland Werke Ag | Wärmeaustauscherrohr und Verfahren zu dessen Herstellung |
US7096931B2 (en) * | 2001-06-08 | 2006-08-29 | Exxonmobil Research And Engineering Company | Increased heat exchange in two or three phase slurry |
US7857037B2 (en) | 2001-11-27 | 2010-12-28 | Thermotek, Inc. | Geometrically reoriented low-profile phase plane heat pipes |
US7198096B2 (en) | 2002-11-26 | 2007-04-03 | Thermotek, Inc. | Stacked low profile cooling system and method for making same |
US6834712B2 (en) * | 2001-11-27 | 2004-12-28 | Thermotek, Inc. | Stacked low profile cooling system and method for making same |
US9113577B2 (en) | 2001-11-27 | 2015-08-18 | Thermotek, Inc. | Method and system for automotive battery cooling |
US20040010913A1 (en) * | 2002-04-19 | 2004-01-22 | Petur Thors | Heat transfer tubes, including methods of fabrication and use thereof |
DE10328748B4 (de) * | 2003-06-25 | 2017-12-14 | Mahle International Gmbh | Wärmeübertrager, insbesondere Ladeluftkühler für Nutzfahrzeuge |
US7254964B2 (en) * | 2004-10-12 | 2007-08-14 | Wolverine Tube, Inc. | Heat transfer tubes, including methods of fabrication and use thereof |
US20070028649A1 (en) * | 2005-08-04 | 2007-02-08 | Chakravarthy Vijayaraghavan S | Cryogenic air separation main condenser system with enhanced boiling and condensing surfaces |
CN100365369C (zh) * | 2005-08-09 | 2008-01-30 | 江苏萃隆铜业有限公司 | 蒸发器热交换管 |
CN100458344C (zh) * | 2005-12-13 | 2009-02-04 | 金龙精密铜管集团股份有限公司 | 一种电制冷满液式机组用铜冷凝换热管 |
CN100437011C (zh) * | 2005-12-13 | 2008-11-26 | 金龙精密铜管集团股份有限公司 | 一种电制冷机组用满液式铜蒸发换热管 |
US8534645B2 (en) * | 2007-11-13 | 2013-09-17 | Dri-Steem Corporation | Heat exchanger for removal of condensate from a steam dispersion system |
CA2644003C (fr) | 2007-11-13 | 2014-09-23 | Dri-Steem Corporation | Systeme de transfert de chaleur comprenant une tuyauterie avec des sites d'ebullition a nucleation |
CN100547339C (zh) * | 2008-03-12 | 2009-10-07 | 江苏萃隆精密铜管股份有限公司 | 一种强化传热管及其制作方法 |
US20090294112A1 (en) * | 2008-06-03 | 2009-12-03 | Nordyne, Inc. | Internally finned tube having enhanced nucleation centers, heat exchangers, and methods of manufacture |
DE102009007446B4 (de) * | 2009-02-04 | 2012-03-29 | Wieland-Werke Ag | Wärmeübertragerrohr und Verfahren zu dessen Herstellung |
CN102130622A (zh) * | 2011-04-07 | 2011-07-20 | 上海威特力焊接设备制造股份有限公司 | 一种高效率光伏逆变器 |
DE102011121733A1 (de) * | 2011-12-21 | 2013-06-27 | Wieland-Werke Ag | Verdampferrohr mit optimierter Außenstruktur |
JP2014072265A (ja) * | 2012-09-28 | 2014-04-21 | Hitachi Ltd | 冷却システム、及びそれを用いた電子装置 |
US20160025010A1 (en) * | 2013-03-26 | 2016-01-28 | United Technologies Corporation | Turbine engine and turbine engine component with cooling pedestals |
JP6198452B2 (ja) * | 2013-05-08 | 2017-09-20 | 株式会社神戸製鋼所 | 中間媒体式気化器 |
US10088180B2 (en) | 2013-11-26 | 2018-10-02 | Dri-Steem Corporation | Steam dispersion system |
US10174960B2 (en) | 2015-09-23 | 2019-01-08 | Dri-Steem Corporation | Steam dispersion system |
DE102016006914B4 (de) | 2016-06-01 | 2019-01-24 | Wieland-Werke Ag | Wärmeübertragerrohr |
US9945618B1 (en) * | 2017-01-04 | 2018-04-17 | Wieland Copper Products, Llc | Heat transfer surface |
US20180292146A1 (en) * | 2017-04-10 | 2018-10-11 | United Technologies Corporation | Partially additively manufactured heat exchanger |
DE102018004701A1 (de) | 2018-06-12 | 2019-12-12 | Wieland-Werke Ag | Metallisches Wärmeaustauscherrohr |
KR102275301B1 (ko) * | 2019-01-28 | 2021-07-08 | 엘지전자 주식회사 | 전열관 및 칠러용 열교환기 |
CN112944993A (zh) * | 2019-12-10 | 2021-06-11 | 珠海格力电器股份有限公司 | 换热管、换热器及空调器 |
JP7164557B2 (ja) * | 2020-02-25 | 2022-11-01 | 株式会社Kmct | 沸騰型伝熱管 |
CN112222217A (zh) * | 2020-09-24 | 2021-01-15 | 上海宇洋特种金属材料有限公司 | T形交叉齿钢带的轧制方法 |
DE202020005628U1 (de) | 2020-10-31 | 2021-11-11 | Wieland-Werke Aktiengesellschaft | Metallisches Wärmeaustauscherrohr |
DE202020005625U1 (de) | 2020-10-31 | 2021-11-10 | Wieland-Werke Aktiengesellschaft | Metallisches Wärmeaustauscherrohr |
KR20230098132A (ko) | 2020-10-31 | 2023-07-03 | 빌란트-베르케악티엔게젤샤프트 | 금속 열교환기 튜브 |
WO2022089772A1 (fr) | 2020-10-31 | 2022-05-05 | Wieland-Werke Ag | Tube métallique d'échangeur de chaleur |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4313248A (en) * | 1977-02-25 | 1982-02-02 | Fukurawa Metals Co., Ltd. | Method of producing heat transfer tube for use in boiling type heat exchangers |
JPS57131992A (en) | 1981-12-24 | 1982-08-16 | Furukawa Electric Co Ltd:The | Nucleate boiling type heat transfer pipe |
EP0222100A2 (fr) * | 1985-10-31 | 1987-05-20 | Wieland-Werke Ag | Tube à ailettes à fond de rainure muni d'encoches et son procédé de fabrication |
US4715433A (en) * | 1986-06-09 | 1987-12-29 | Air Products And Chemicals, Inc. | Reboiler-condenser with doubly-enhanced plates |
EP0305632A1 (fr) * | 1985-06-12 | 1989-03-08 | Wolverine Tube, Inc. (Alabama) | Méthode de fabrication d'un tube de transfert de chaleur |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3326283A (en) * | 1965-03-29 | 1967-06-20 | Trane Co | Heat transfer surface |
US4074753A (en) * | 1975-01-02 | 1978-02-21 | Borg-Warner Corporation | Heat transfer in pool boiling |
JPS5211465A (en) * | 1975-07-18 | 1977-01-28 | Hitachi Cable Ltd | Boiling heat conduction pipe |
DE2808080C2 (de) * | 1977-02-25 | 1982-12-30 | Furukawa Metals Co., Ltd., Tokyo | Wärmeübertragungs-Rohr für Siedewärmetauscher und Verfahren zu seiner Herstellung |
US4549606A (en) * | 1982-09-08 | 1985-10-29 | Kabushiki Kaisha Kobe Seiko Sho | Heat transfer pipe |
JPS5993190A (ja) * | 1982-11-17 | 1984-05-29 | Hitachi Ltd | 熱交換壁 |
US4733698A (en) * | 1985-09-13 | 1988-03-29 | Kabushiki Kaisha Kobe Seiko Sho | Heat transfer pipe |
SU1384912A1 (ru) * | 1986-10-28 | 1988-03-30 | Производственное Объединение "Белгородский Завод Энергетического Машиностроения" | Теплообменна труба |
-
1991
- 1991-01-14 JP JP3014857A patent/JP2788793B2/ja not_active Expired - Lifetime
- 1991-12-30 KR KR1019910025550A patent/KR940007194B1/ko not_active IP Right Cessation
-
1992
- 1992-01-13 US US07/819,242 patent/US5186252A/en not_active Expired - Lifetime
- 1992-01-14 DE DE69200089T patent/DE69200089T2/de not_active Revoked
- 1992-01-14 EP EP92100503A patent/EP0495453B1/fr not_active Revoked
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4313248A (en) * | 1977-02-25 | 1982-02-02 | Fukurawa Metals Co., Ltd. | Method of producing heat transfer tube for use in boiling type heat exchangers |
JPS57131992A (en) | 1981-12-24 | 1982-08-16 | Furukawa Electric Co Ltd:The | Nucleate boiling type heat transfer pipe |
EP0305632A1 (fr) * | 1985-06-12 | 1989-03-08 | Wolverine Tube, Inc. (Alabama) | Méthode de fabrication d'un tube de transfert de chaleur |
EP0222100A2 (fr) * | 1985-10-31 | 1987-05-20 | Wieland-Werke Ag | Tube à ailettes à fond de rainure muni d'encoches et son procédé de fabrication |
US4715433A (en) * | 1986-06-09 | 1987-12-29 | Air Products And Chemicals, Inc. | Reboiler-condenser with doubly-enhanced plates |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0559599A1 (fr) * | 1992-03-02 | 1993-09-08 | Carrier Corporation | Tube pour échangeur de chaleur |
EP0607839A1 (fr) * | 1993-01-22 | 1994-07-27 | Wieland-Werke Ag | Tube pour échange de chaleur, procédé de fabrication et utilisation d'un tel tube |
CN101532795B (zh) * | 2008-03-12 | 2013-07-24 | 威兰德-沃克公开股份有限公司 | 金属热交换管 |
CN101776412A (zh) * | 2010-03-02 | 2010-07-14 | 金龙精密铜管集团股份有限公司 | 蒸发传热管 |
CN101776412B (zh) * | 2010-03-02 | 2012-11-21 | 金龙精密铜管集团股份有限公司 | 蒸发传热管 |
WO2014072046A1 (fr) * | 2012-11-12 | 2014-05-15 | Wieland-Werke Ag | Tube de transfert de chaleur par évaporation doté d'une cavité creuse |
US9541336B2 (en) | 2012-11-12 | 2017-01-10 | Wieland-Werke Ag | Evaporation heat transfer tube with a hollow cavity |
WO2015128061A1 (fr) * | 2014-02-27 | 2015-09-03 | Wieland-Werke Ag | Tube d'échangeur de chaleur métallique |
CN106030233A (zh) * | 2014-02-27 | 2016-10-12 | 威兰德-沃克公开股份有限公司 | 金属热交换器管 |
US20160305717A1 (en) * | 2014-02-27 | 2016-10-20 | Wieland-Werke Ag | Metal heat exchanger tube |
US11073343B2 (en) | 2014-02-27 | 2021-07-27 | Wieland-Werke Ag | Metal heat exchanger tube |
Also Published As
Publication number | Publication date |
---|---|
KR940007194B1 (ko) | 1994-08-08 |
JP2788793B2 (ja) | 1998-08-20 |
DE69200089D1 (de) | 1994-05-11 |
DE69200089T2 (de) | 1994-09-01 |
JPH04236097A (ja) | 1992-08-25 |
US5186252A (en) | 1993-02-16 |
EP0495453B1 (fr) | 1994-04-06 |
KR920015114A (ko) | 1992-08-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0495453B1 (fr) | Tube pour la transmission de chaleur | |
US6164370A (en) | Enhanced heat exchange tube | |
US4159739A (en) | Heat transfer surface and method of manufacture | |
US5803165A (en) | Heat exchanger | |
EP0499257B1 (fr) | Tube de petite dimension pour transfert de chaleur et sa méthode de fabrication | |
EP0603108B1 (fr) | Tube d'échangeur de chaleur | |
US5669441A (en) | Heat transfer tube and method of manufacture | |
US6913073B2 (en) | Heat transfer tube and a method of fabrication thereof | |
EP1502067B1 (fr) | Tubes de transfert de chaleur, et procedes de fabrication et d'utilisation de ces derniers | |
US5333682A (en) | Heat exchanger tube | |
US5996686A (en) | Heat transfer tubes and methods of fabrication thereof | |
US5832995A (en) | Heat transfer tube | |
US4938282A (en) | High performance heat transfer tube for heat exchanger | |
US4195688A (en) | Heat-transfer wall for condensation and method of manufacturing the same | |
JP3947158B2 (ja) | 熱交換器 | |
US5010643A (en) | High performance heat transfer tube for heat exchanger | |
JPS6011800B2 (ja) | 凝縮伝熱管の製造法 | |
US2162694A (en) | Process of making a heat exchanging element | |
SU1828535A3 (ru) | Teплooбmehhиk | |
JP4587545B2 (ja) | 吸収器用伝熱管 | |
JP2737799B2 (ja) | 伝熱管 | |
JP2773872B2 (ja) | 沸騰・凝縮用伝熱管 | |
JP3129565B2 (ja) | 熱交換器用伝熱管 | |
JPH0615950B2 (ja) | 液―液式熱交換器用伝熱管 | |
JP3019699B2 (ja) | 管内吸収用伝熱管 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19920114 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE FR GB IT |
|
17Q | First examination report despatched |
Effective date: 19930119 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE FR GB IT |
|
ITF | It: translation for a ep patent filed | ||
REF | Corresponds to: |
Ref document number: 69200089 Country of ref document: DE Date of ref document: 19940511 |
|
ET | Fr: translation filed | ||
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
26 | Opposition filed |
Opponent name: WIELAND-WERKE AG Effective date: 19941222 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19960105 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19960109 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19960115 Year of fee payment: 5 |
|
RDAG | Patent revoked |
Free format text: ORIGINAL CODE: 0009271 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: PATENT REVOKED |
|
27W | Patent revoked |
Effective date: 19960107 |
|
GBPR | Gb: patent revoked under art. 102 of the ep convention designating the uk as contracting state |
Free format text: 960107 |